US8299282B2 - Continuous method for the heterogenically catalyzed esterification of fatty acids - Google Patents

Continuous method for the heterogenically catalyzed esterification of fatty acids Download PDF

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Publication number
US8299282B2
US8299282B2 US12/738,115 US73811508A US8299282B2 US 8299282 B2 US8299282 B2 US 8299282B2 US 73811508 A US73811508 A US 73811508A US 8299282 B2 US8299282 B2 US 8299282B2
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process according
fatty acids
free fatty
catalyst
alcohol
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US20100249442A1 (en
Inventor
Dieter Heinz
Leslaw Mleczko
Shaibal Roy
Heinrich Morhenn
Wulf Dietrich
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Rohm and Haas Chemicals LLC
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Bayer Technology Services GmbH
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    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C67/00Preparation of carboxylic acid esters
    • C07C67/03Preparation of carboxylic acid esters by reacting an ester group with a hydroxy group
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C67/00Preparation of carboxylic acid esters
    • C07C67/08Preparation of carboxylic acid esters by reacting carboxylic acids or symmetrical anhydrides with the hydroxy or O-metal group of organic compounds
    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11CFATTY ACIDS FROM FATS, OILS OR WAXES; CANDLES; FATS, OILS OR FATTY ACIDS BY CHEMICAL MODIFICATION OF FATS, OILS, OR FATTY ACIDS OBTAINED THEREFROM
    • C11C3/00Fats, oils, or fatty acids by chemical modification of fats, oils, or fatty acids obtained therefrom
    • C11C3/003Fats, oils, or fatty acids by chemical modification of fats, oils, or fatty acids obtained therefrom by esterification of fatty acids with alcohols
    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11CFATTY ACIDS FROM FATS, OILS OR WAXES; CANDLES; FATS, OILS OR FATTY ACIDS BY CHEMICAL MODIFICATION OF FATS, OILS, OR FATTY ACIDS OBTAINED THEREFROM
    • C11C3/00Fats, oils, or fatty acids by chemical modification of fats, oils, or fatty acids obtained therefrom
    • C11C3/04Fats, oils, or fatty acids by chemical modification of fats, oils, or fatty acids obtained therefrom by esterification of fats or fatty oils
    • C11C3/10Ester interchange
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/10Biofuels, e.g. bio-diesel

Definitions

  • DE 196 00 025 discloses, inter alia, that it may be advantageous to add additional free fatty acids to the pre-esterification. Under some circumstances, this can serve to reduce the relative proportion by mass of inert material in the starting material of the process.
  • no fundamental solution to the technical problem of achieving higher conversions and consequent increased space-time yields of a pre-esterification is disclosed, since, more particularly, the free fatty acids used for the increase in the proportion of the free fatty acids preferably stem from a later process step and are therefore subjected to further processing steps. This is especially true because soap cleavage by means of metered addition of homogeneously dissolved acids becomes necessary here.
  • the maximum space-time yield disclosed in DE 196 00 025 is 34 g of fatty acid methyl ester per litre of reactor volume and hour.
  • starting materials are all fats and/or oils which include at least a proportion of free fatty acids, and a proportion of fatty acid glycerides. Preference is given to starting materials which possess a proportion of free fatty acids greater than 2% by weight.
  • alcohols refer to mono- or polyhydric C 1 to C 5 alcohols or mixtures thereof Preference is given to monohydric C 1 to C 3 alcohols. Very particular preference is given to methanol.
  • the hydricity of an alcohol describes the number of covalently bonded hydroxyl groups present in the inventive alcohol.
  • the conversion of free fatty acids at the outlet of the second reaction stage is at least 90% based on the stream from the first reaction stage ( 5 ) and at least 99.5% based on the stream into the first reaction stage ( 3 ).
  • the stream ( 9 ) of the free fatty acids which have thus been converted to alkyl esters is added, in a mixer ( 60 ), in step 6) of the process according to the invention, to the stream ( 11 ) of starting material which stems from the reaction stage ( 20 ) for transesterification and has likewise been converted to alkyl esters, so as to obtain, for example, a stream of biodiesel ( 12 ).

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Wood Science & Technology (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
  • Fats And Perfumes (AREA)
  • Catalysts (AREA)
US12/738,115 2007-10-30 2008-10-16 Continuous method for the heterogenically catalyzed esterification of fatty acids Expired - Fee Related US8299282B2 (en)

Applications Claiming Priority (4)

Application Number Priority Date Filing Date Title
DE102007052065 2007-10-30
DE102007052065A DE102007052065A1 (de) 2007-10-30 2007-10-30 Kontinuierliches Verfahren zur heterogen katalysierten Veresterung von Fettsäuren
DE102007052065.6 2007-10-30
PCT/EP2008/008763 WO2009056231A1 (de) 2007-10-30 2008-10-16 Kontinuierliches verfahren zur heterogen katalysierten veresterung von fettsäuren

Publications (2)

Publication Number Publication Date
US20100249442A1 US20100249442A1 (en) 2010-09-30
US8299282B2 true US8299282B2 (en) 2012-10-30

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US12/738,115 Expired - Fee Related US8299282B2 (en) 2007-10-30 2008-10-16 Continuous method for the heterogenically catalyzed esterification of fatty acids

Country Status (22)

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US (1) US8299282B2 (OSRAM)
EP (1) EP2205708A1 (OSRAM)
CN (1) CN101842471B (OSRAM)
AR (1) AR071058A1 (OSRAM)
AU (1) AU2008318001A1 (OSRAM)
BR (1) BRPI0819144A8 (OSRAM)
CA (1) CA2703813A1 (OSRAM)
CO (1) CO6270372A2 (OSRAM)
CR (1) CR11400A (OSRAM)
DE (1) DE102007052065A1 (OSRAM)
EA (1) EA018797B1 (OSRAM)
HN (1) HN2010000893A (OSRAM)
IL (1) IL204938A (OSRAM)
MX (1) MX2010004519A (OSRAM)
NI (1) NI201000073A (OSRAM)
NZ (1) NZ584970A (OSRAM)
PA (1) PA8799301A1 (OSRAM)
PE (1) PE20090934A1 (OSRAM)
SV (1) SV2010003551A (OSRAM)
UY (1) UY31390A1 (OSRAM)
WO (1) WO2009056231A1 (OSRAM)
ZA (1) ZA201002942B (OSRAM)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8957242B2 (en) 2013-03-15 2015-02-17 Renewable Energy Group, Inc. Dual catalyst esterification

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP2522712A1 (en) * 2011-05-13 2012-11-14 Cognis IP Management GmbH Process for obtaining fatty acid lower alkyl esters from unrefined fats and oils
US9738842B2 (en) * 2013-06-19 2017-08-22 Argent Energy (Uk) Limited Process and apparatus for purifying a fatty mixture and related products including fuels
FR3015515B1 (fr) 2013-12-19 2016-02-05 IFP Energies Nouvelles Procede de pretraitement d'huiles vegetales par catalyse heterogene de l'esterification des acides gras

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB384715A (en) * 1931-08-31 1932-12-15 Ig Farbenindustrie Ag Apparatus for carrying out the manufacture and production of neutral products from oiats
DE1960002A1 (de) 1968-12-04 1970-06-18 Jean Joseph Alfred Beyl Sicherheitsskibindung
GB2145079A (en) * 1983-08-17 1985-03-20 Nisshin Oil Mills Ltd Methyl-esterification of deodorisation distillates of oils
EP0192035A2 (de) 1985-01-21 1986-08-27 Henkel Kommanditgesellschaft auf Aktien Verfahren zur Vorveresterung freier Fettsäuren in Rohfetten und/oder -ölen
DE19600025A1 (de) 1996-01-03 1997-07-10 Henkel Kgaa Verfahren zur Herstellung von Fettstoffen
US20050113589A1 (en) * 2003-10-14 2005-05-26 Kao Corporation Process for producing a fatty acid ester
WO2007083213A2 (en) 2006-01-19 2007-07-26 Merloni Progetti S.P.A. Process for the preparation of biodiesel
WO2007093326A1 (en) 2006-02-15 2007-08-23 Aser S.R.L. Method for deacidifying oils and/or fats

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1865401A (zh) * 2006-06-19 2006-11-22 菏泽华瑞油脂有限责任公司 高酸价棉籽油制取生物柴油的方法
CN101016473B (zh) * 2007-03-02 2012-04-18 安徽省粮油科学研究所 劣质油生产生物燃料油的方法
CN101058734B (zh) * 2007-05-31 2010-12-01 张付舜 工业化微波合成生物柴油的装置及其方法

Patent Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB384715A (en) * 1931-08-31 1932-12-15 Ig Farbenindustrie Ag Apparatus for carrying out the manufacture and production of neutral products from oiats
DE1960002A1 (de) 1968-12-04 1970-06-18 Jean Joseph Alfred Beyl Sicherheitsskibindung
GB2145079A (en) * 1983-08-17 1985-03-20 Nisshin Oil Mills Ltd Methyl-esterification of deodorisation distillates of oils
EP0192035A2 (de) 1985-01-21 1986-08-27 Henkel Kommanditgesellschaft auf Aktien Verfahren zur Vorveresterung freier Fettsäuren in Rohfetten und/oder -ölen
US4698186A (en) 1985-01-21 1987-10-06 Henkel Kommanditgesellschaft Auf Aktien Process for the pre-esterification of free fatty acids in fats and oils
DE19600025A1 (de) 1996-01-03 1997-07-10 Henkel Kgaa Verfahren zur Herstellung von Fettstoffen
US20050113589A1 (en) * 2003-10-14 2005-05-26 Kao Corporation Process for producing a fatty acid ester
WO2007083213A2 (en) 2006-01-19 2007-07-26 Merloni Progetti S.P.A. Process for the preparation of biodiesel
WO2007093326A1 (en) 2006-02-15 2007-08-23 Aser S.R.L. Method for deacidifying oils and/or fats

Non-Patent Citations (5)

* Cited by examiner, † Cited by third party
Title
Athanassiadis, A., et al., The deacidification of Vegetable oils by distillation during deodorization, 1988, Fat. Sci. Technol., vol. 90, No. 13, pp. 522-526. *
DIN EN ISO 2114 Plastics (polyester resins) and paints and varnishes (binders)-Determination of partial acid value and total acid value (ISO 2114:2000).
Henkel KGGA, Preparation of fatty acids with low acid values, useful as precursors for esterification, 1997, English translation of DE19600025, 11 pages. *
Martinello, M., et al., Grape seed oil deacidification by molecular distillation: Analysis of operative variables influence using the response surfact methodology, 2006, Journal of Food Engineering, vol. 81. pp. 60-64. *
Mittelbach, Remschmidt, Biodiesel-The comprehensive handbook 3rd ed., 2006, p. 60.

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8957242B2 (en) 2013-03-15 2015-02-17 Renewable Energy Group, Inc. Dual catalyst esterification

Also Published As

Publication number Publication date
NI201000073A (es) 2010-09-23
US20100249442A1 (en) 2010-09-30
PA8799301A1 (es) 2009-06-23
PE20090934A1 (es) 2009-07-24
IL204938A (en) 2013-12-31
HN2010000893A (es) 2013-06-24
CN101842471B (zh) 2014-12-10
ZA201002942B (en) 2011-07-27
EP2205708A1 (de) 2010-07-14
BRPI0819144A8 (pt) 2016-04-26
BRPI0819144A2 (OSRAM) 2009-05-07
AU2008318001A1 (en) 2009-05-07
DE102007052065A1 (de) 2009-05-07
EA018797B1 (ru) 2013-10-30
CN101842471A (zh) 2010-09-22
CA2703813A1 (en) 2009-05-07
AR071058A1 (es) 2010-05-26
UY31390A1 (es) 2009-05-29
WO2009056231A1 (de) 2009-05-07
CR11400A (es) 2010-11-02
NZ584970A (en) 2012-06-29
CO6270372A2 (es) 2011-04-20
SV2010003551A (es) 2011-08-11
MX2010004519A (es) 2010-05-14
EA201000582A1 (ru) 2010-10-29
IL204938A0 (en) 2010-11-30

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